Oxygen Generating Compositions Comprising (Fe,Mg)O

ABSTRACT

The present disclosure provides an oxygen-generating composition comprising an oxygen source and a mixed-metal oxide of formula: (Fe,Mg)O.

FOREIGN PRIORITY

This application claims priority to German Patent Application No.102015117835.4 filed 20 Oct. 2015, the entire contents of which isincorporated herein by reference.

TECHNICAL FIELD

The present disclosure relates to oxygen-generating compositions anddevices, i.e. chemical oxygen generators, as well as methods for theirpreparation.

BACKGROUND

Chemical oxygen generators are used for emergency systems, e.g. inaircraft, breathing apparatus for emergency services such asfire-fighters and mine rescue crews, in submarines, and other situationsin which a compact emergency oxygen generator with a long shelf life isneeded. They release oxygen via a chemical reaction, typical oxygensources being inorganic, especially alkaline metal or alkaline earthmetal, superoxides, chlorates, or perchlorates.

Chlorate candles, also known as oxygen candles, are examples of chemicaloxygen generators that use chlorates or perchlorates as the oxygensource. Chlorate candles can produce oxygen at a fixed rate at about 6.5man-hours of oxygen per kilogram of the mixture and have a long shelflife.

In addition to the oxygen-delivering compounds, additives with differentproperties are used in chemical oxygen generators, for example: fuels,catalysts, binders and moderators. Fuels support the oxygen-producingreaction and are typically metal powders, e.g. powders of iron, tin,manganese, cobalt, nickel, tungsten, titanium, magnesium, aluminium,niobium, zirconium, and/or mixtures thereof.

Transition metal oxides are typically used to catalyse the exothermicoxygen-producing reaction, particularly to reduce the temperature atwhich it takes place and thus reduce the heat released by the device inaction. A commonly used catalyst is cobalt oxide, due to its ability toreduce the temperature of the decomposition reaction, e.g. of sodiumchlorate to 290-400° C. Cobalt oxide is however, toxic and expensive,and thus it is necessary to use it in very low amounts. Althougheffective at low amounts (e.g. 0.1 wt. %), achieving uniform mixing atsuch low concentrations is difficult. Non-uniform mixing results inerratic performance, such as non-uniform oxygen production, which isclearly undesirable. Other commonly-used catalysts are manganese oxides,although these can produce high concentrations of chlorine in the oxygenproduced. There thus exists a need to provide alternative catalysts foroxygen generation which overcome these problems.

Chemical oxygen generators are required to produce an enduring andcontinuous oxygen flow. For this reason, moderators are also used, i.e.to avoid unwanted side reaction products like chlorine during thedecomposition process and/or to ensure a sufficient and substantiallyuniform oxygen flow. BaO2 is often used as a moderator, but this istoxic and thus disposal of scrap is expensive.

Chemical oxygen generators, i.e. chemical oxygen-generating devices,usually comprise moulds, i.e. containers or pellets which comprise thechemicals; these moulds, containers or pellets obviously need to remainstructurally stable before and during use of the oxygen generator inorder to avoid failure during the initial firing process and to avoidinterruption of oxygen flow which could occur due to any mechanicalchanges of the generator body induced by environmental effects or thereaction's progress. Binders are therefore used in order to stabilisethe body of the chemical oxygen generator, e.g. the chlorate candlebody, and ensure that it remains safe during use. Typical binders aremica, glass powder, glass fibre, fibreglass, ceramic fibre, bentonite,kaolinite and mixtures thereof, although other inorganic binders canalso be suitable. These add undesirable extra bulk to the compositionsused to produce oxygen.

Decomposition of chlorates to release oxygen is exothermic, for examplesodium chlorate decomposes at 500 to 600° C. Due to the hightemperatures involved, chemical oxygen generators require thermalinsulation to protect surrounding equipment. Such insulation addsfurther bulk to the oxygen generator, which is clearly undesirable asthey may need to be stored for long periods, usually in locations (e.g.aircraft, submarines, fire engines) where space and weight capacity arelimited. There is thus a need to reduce the size and/or weight of oxygengenerators.

The present inventors have surprisingly found that certain oxidecompounds are multi-functional, acting as catalyst, binder and fuel.These compounds therefore enable the production of lighter and morecompact oxygen generators. Moreover, as the compounds are non-toxic, theabove-mentioned problems with commonly used toxic catalysts are alsoavoided.

Thus, viewed from a first aspect, the present disclosure provides anoxygen-generating composition comprising an oxygen source and amixed-metal oxide of formula: (Fe,Mg)O. Preferably the mixed-metal oxideis in the form of nano-particles.

The degree of crystallinity of the mixed-metal oxides can be increasedby thermal treatment, e.g. calcination. However, the best catalyticperformance has been found for oxides of the present disclosure whichare non-crystalline, e.g. semi-crystalline or amorphous. The oxides ofthe present disclosure are therefore preferably uncalcinated, i.e. theyhave not been thermally treated such that the degree of crystallinity isincreased.

Preferably less than 90% (e.g. wt. %), especially less than 75%,particularly less than 50%, especially preferably less than 25% or lessthan 10% of the mixed-metal oxide material described herein iscrystalline. Especially preferably the mixed-metal oxide of formula:(Fe,Mg)O is substantially semi-crystalline or substantially amorphous.

Crystallinity can be measured using X-ray diffraction (XRD) or any othertechniques known in the art, such as differential scanning calorimetry.Crystallinity involves both a short-range and long-range order ofperiodically occurring atoms inside the crystal lattice which results incharacteristic well-defined X-ray powder patterns. Mixed-metal oxides offormula: (Fe,Mg)O which have not been subjected to thermal treatmentexhibit low degrees of crystallinity and can be referred to as amorphousor semi-crystalline. Such materials contain only short-range order ofthe atoms which results in undefined X-ray powder patterns which lackthe significant reflexes found for more crystalline forms.

Preferably the mixed-metal oxide as herein described is in the form of apowder. Especially preferably the mixed-metal oxide is in the form ofnano-particles, e.g. a nano-particulate powder.

The notation “(Fe,Mg)O” is intended to denote a single chemical entity,rather than, for example, a mixture of iron oxide(s) and magnesiumoxide(s). The compositions of the present disclosure therefore comprisea mixed-metal iron-magnesium oxide, rather than a mixture of these metaloxides. The oxide of the present disclosure can therefore be viewed asFe-doped MgO, i.e. MgO in which some magnesium cations are substitutedby iron cations in the crystal lattice. Although the oxide could bedoped FeO, doping of MgO is, however, most preferred. In the oxides ofthe present disclosure, iron typically has an oxidation state of +2and/or +3.

The content of each element may be determined by standard techniques,e.g. atomic absorption spectroscopy or inductively coupled plasma atomicemission spectroscopy. Preferred examples of the mixed-metal oxides ofthe present disclosure are (Fe,Mg)O, where the iron content is 0.01 to30 Atom % (at. %), especially 0.05 to 5 at. %, especially preferably 0.5to 5 at. %, e.g. around 3 at. %. Other preferred ranges for the ironcontent are 1 to 10 at. %, preferably 2 to 8 at. %, e.g. 3 to 6 at %.

An alternative notation would be (Fex,Mg1-x)O, where x is preferably0.0002 to 0.6; especially 0.001 to 0.1, especially preferably 0.01 to0.1, e.g. around 0.06.

Thermal treatment below <1050° C. does not change the relativeproportions of the metals.

The inventors have developed a process for producing the mixed-metaloxides of the present disclosure in nano-particulate form. The use of(or method of using) such nano-particles in oxygen production, e.g. asbinders, fuels and/or catalysts/moderators in oxygen production, forms afurther novel aspect of this disclosure. Thus, in a preferred aspect,the mixed-metal oxides herein described are in the form of particleshaving a diameter (e.g. the average particle diameter) of less than orequal to 500 nm, preferably less than or equal to 300 nm, especiallyless than or equal to 200 nm. Smaller particles allow for better mixingin oxygen-generating compositions and thus more uniform oxygenproduction.

The mixed-metal oxides of the present disclosure may be characterisedusing standard techniques, such as surface area analysis, absorptionspectroscopy, inductively coupled plasma atomic emission spectroscopy,X-ray diffraction, electron paramagnetic resonance nuclear magneticresonance, scanning electron microscopy and/or transmission electronmicroscopy.

The specific surface area of the mixed-metal oxide materials of thepresent disclosure may be determined using standard techniques, e.g. aSurface Area Analyzer with surface areas calculable by the method ofBrunauer, Emmett and Teller. Typical BET surface areas are 5 to 50 m2/g,e.g. 10 to 40 m2/g, especially 25 to 35 m2/g.

Characterisation of the oxides by X-ray diffraction (XRD) is possibleusing standard techniques, e.g. CuKα1 radiation, with a wavelength 0.154nm.

EPR experiments may be performed in conventional continuous wave (cw) aswell as in pulsed mode.

In some aspects, the mixed-metal oxide can form up to 70 wt. % of theoxygen-generating composition, i.e. the composition may comprise 0.1 to70 wt. %, preferably 0.1 to 10 wt. %, particularly preferably 0.2 to 5wt. %, e.g. 2 to 4 wt. %, especially around 3 wt. % mixed-metal oxide asherein described, where the amount of mixed-metal oxide is expressed asweight percent of the oxygen-generating composition as a whole (i.e.regarding the total weight of the oxygen source, mixed-metal oxide andany other components).

The oxygen source may be any compound suitable for producing breathableoxygen. Metal (especially alkali metal or alkaline earth metal)halogenates (especially chlorates, perchlorates or mixtures thereof),peroxides or superoxides are suitable, especially those of lithium,sodium or potassium, e.g. KO2. Preferably the oxygen source is, orcomprises, one or more compounds selected from alkali metal chlorates,alkali metal perchlorates, alkaline earth metal chlorates, alkalineearth metal perchlorates and mixtures thereof, especially preferablyalkali metal chlorates and/or alkali metal perchlorates. Particularlypreferred oxygen sources are those comprising sodium or lithium,particularly sodium chlorate and lithium perchlorate, e.g. the oxygensource is preferably sodium chlorate and/or lithium perchlorate.

The oxygen-generating composition of the disclosure typically comprises30 to 99.9 wt. % oxygen source, preferably 40 to 99 wt. %, especiallypreferably 70 to 99 wt. %, e.g. at least 80 wt. % or at least 95 wt. %,especially 90 to 99.9 wt. % where the amount of oxygen source isexpressed as weight percent of the oxygen-generating composition as awhole (i.e. regarding the total weight of the oxygen source, mixed-metaloxide and any other components).

It is a particularly preferred aspect of all embodiments of thisdisclosure that the oxygen produced is breathable, e.g. without furthertreatment.

As discussed further in the Examples, it has been surprisingly foundthat the mixed-metal oxides of the present disclosure aremultifunctional, acting as a catalyst as well as a fuel and binder.Thus, there is no need for additional fuel, binder, catalyst ormoderator components in the oxygen-generating compositions of thepresent disclosure. This means that the compositions are simpler,quicker and cheaper to produce than conventional oxygen-generatingcompositions and that they are more compact and weigh less than those ofthe prior art (which require separate fuel, binder, catalyst and/ormoderator components). This results in lighter and more compactoxygen-generators, e.g. chlorate candles. Yet further space and costsavings are enabled by the reduction in thermal insulation required foroxygen generators using the compositions of the present disclosure—lessinsulation being required due to a reduction in temperature of theoxygen-producing reaction due to the catalytic properties of themixed-metal oxides disclosed herein. Moreover, the mixed-metal oxides ofthe present disclosure are non-toxic and enable more uniform oxygenproduction due to the more efficient mixing possible due to theirnano-particulate nature.

For example, (Fe,Mg)O has been found to perform better as a catalystthan other non-toxic catalysts such as Fe(III)oxide. Furthermore, themixed-metal oxide of the present disclosure also acts as a binder andfuel, thus removing the need for further components to perform thesefunctions and is non-toxic, and so preferable to cobalt oxide, which iscommonly considered to be the best catalyst for this type of reaction.

Due to the multi-functional nature of the oxides herein described, theoxygen-generating compositions do not require the presence of separatefuels, catalysts, moderators or binders. Preferably the compositions asherein described therefore consist of, or consist essentially of the(one or more, preferably one) oxygen source and (one or more, preferablyone of the) mixed-metal oxide described herein. However, although thecompositions of the present disclosure do not require the presence offurther components, one or more additional components may be present.Thus, one aspect of the present disclosure relates to the compositionsas herein described additionally comprising one or more additives, e.g.fuels, catalysts, moderators and/or binders.

Thus, the compositions as herein described may further comprise one ormore fuels. Metals or non-metals such as silicon, boron and/or carbonmay be used. Preferably the fuel is in powder form, especially a metalpowder, e.g. a powder of, or comprising, iron, tin, manganese, cobalt,nickel, tungsten, titanium, magnesium, aluminium, niobium or zirconiumand/or mixtures thereof. The compositions may optionally comprise 0 to 5(e.g. 0.1 to 5) wt. % of such fuel (expressed as the weight percentageof the total weight of additional fuels as part of the composition as awhole), preferably 0 to 1 (e.g. 0.1 to 1) wt. %, especially 0 to 0.5(e.g. 0.1 to 0.5) wt. %.

The compositions as herein described may further comprise one or morecatalysts, e.g. a transition metal oxide, preferably selected frommanganese oxides (e.g. MnO, Mn2O3), iron oxides (e.g. FeO and/or Fe2O3)cobalt oxide, copper oxide, nickel oxide and mixtures thereof. Thecompositions may optionally comprise 0 to 5 (e.g. 0.1 to 5) wt. % ofsuch catalyst (expressed as the weight percentage of the total weight ofadditional catalysts as part of the composition as a whole), preferably0 to 1 (e.g. 0.1 to 1) wt. %, especially 0 to 0.5 (e.g. 0.1 to 0.5) wt.%.

The compositions as herein described may further comprise one or moremoderators, e.g. chlorine removers and/or reaction rate modifiers (e.g.inhibitors). These are preferably selected from the oxides, peroxidesand hydroxides of alkali and alkaline earth metals, preferably bariumperoxide. These compounds serve for binding chlorine and carbon dioxide,which are sometimes produced in trace amounts, but should not be presentin breathable oxygen. They can also moderate the production of oxygen,ensuring a uniform supply. The compositions may optionally comprise 0 to5 (e.g. 0.1 to 5) wt. % of such moderators (expressed as the weightpercentage of the total weight of additional moderators as part of thecomposition as a whole), preferably 0 to 1 (e.g. 0.1 to 1) wt. %,especially 0 to 0.5 (e.g. 0.1 to 0.5) wt. %.

The compositions as herein described may further comprise one or morebinders, preferably selected from inorganic binders such as mica, glasspowder, glass fibre, fibreglass, ceramic fibre, steel wool, bentonite,kaolinite and mixtures thereof, for example, although other inorganicbinders can also be suitable.

The oxygen-generating compositions as herein described may be made bycombining the oxygen source with the mixed-metal oxide (and any otheroptional components). The disclosure therefore also provides a methodfor preparing an oxygen-generating composition as herein described, saidmethod comprising combining the oxygen source with the mixed-metaloxide. Optionally the oxygen source is mixed with, e.g. 1-5 wt. %, waterprior to being combined with the mixed-metal oxide. If any of theadditional components mentioned herein are desired to be present in thecomposition, these would typically be mixed together with themixed-metal oxide, preferably prior to combination with the oxygensource. The components may be combined by any suitable method, e.g.mixing. After the components have been combined, the resultingoxygen-generating composition may be dried and stored for future use, orplaced in a mould to form part of an oxygen generator.

The mixed-metal oxide of the present disclosure may be prepared by anyknown route. Suitable routes for the manufacture of oxides of this typeare found in Top. Catal. (2011) 54; 1266-1285. Most preferably, themixed-metal oxide is prepared by co-precipitation, e.g. by addingaqueous solutions of salts such as Mg(NO3)2.6H2O and Fe(NO3)3.9H2O to asolution, preferably an ammonia solution (preferably at a pH of 11 orabove) to precipitate a semi-crystalline powder.

Other metal salts, e.g. chlorides or phosphates may be used for theprecipitation step, but nitrates are especially preferred as they arecompletely removable by thermal treatment. Similarly, ammonia is thepreferred medium for precipitation. If chlorides are used, theprecipitate may need to be extensively washed to avoid the presence ofchlorine.

In order to produce nano-particles, the resulting material may bequick-frozen using liquid N2, followed by freeze-drying, e.g. for over12 hours, especially over 72 hours. The combination of precipitation,freezing and freeze-drying produces homogenous, high puritynano-particles.

Decomposition of the oxygen source of the compositions of the presentdisclosure results in oxygen production. Thus, viewed from a furtheraspect, the present disclosure provides the use of a mixed-metal oxideas herein described in a method for generating oxygen. The presentdisclosure also provides use of the mixed-metal oxides as hereindescribed as multi-functional components in oxygen-generatingcompositions and oxygen generators, i.e. a single component with thefunctions of catalyst, binder and fuel. A further aspect of the presentdisclosure relates to a method for generating oxygen, said methodcomprising decomposing an oxygen source as herein described in thepresence of a mixed-metal oxide as herein described.

The compositions of the present disclosure have utility in chemicaloxygen generators, also referred to as “chemical oxygen generatingdevices”, “chemical oxygen systems”, “chemical oxygen generatingsystems”, “oxygen-generators” etc.

Thus, viewed from a further aspect, the present disclosure provides achemical oxygen generator comprising an oxygen-generating composition asherein described. Preferably, said generator comprises a container forcontaining the oxygen-generating composition and a primer for startingdecomposition of the oxygen-generating composition.

Typical chemical oxygen generators/devices according to the presentdisclosure are fixed chemical oxygen generators and portable chemicaloxygen generators. Especially preferably the chemical oxygen generatoris, or comprises, a chlorate candle.

Fixed chemical oxygen generators are used in fixed systems, e.g. thosecommonly used in passenger-carrying aircraft. The system typicallycomprises boxes, each carrying an oxygen generator and one or morepassenger masks. The generators are activated as the masks arepresented. Thus, the present disclosure also provides the use of thecompositions and generators as herein described in a fixed oxygengeneration system, e.g., an aircraft oxygen generation system. Thepresent disclosure also provides a method for producing oxygen, e.g. inan aircraft, comprising use of the compositions and generators as hereindescribed.

Aircraft typically carry one or more oxygen generating systems selectedfrom continuous flow systems, demand flow systems, diluter demandsystems and pressure demand systems. The generators and compositions ofthe present disclosure may be used in any such system. Thus, a furtheraspect of the disclosure provides an oxygen generating system,preferably an aircraft oxygen generating system, comprising a chemicaloxygen generator or oxygen generating compositions as herein described.

The present disclosure also provides a kit for making anoxygen-generating composition as herein described or a kit for making achemical oxygen generator as herein described, said kit comprising anoxygen source as herein described and a mixed-metal oxide as hereindescribed.

Chemical oxygen-generating devices such as chlorate candles typicallyhave a generally cylindrical shape with a taper, with a recess at oneend to hold an ignition pellet. A typical candle configuration is shownin FIG. 1 of SAE AIR1133. The ignition pellet may be ignited by firing aprimer. The heat from the ignition pellet then ignites the reaction ofthe candle body and generates oxygen. The oxygen-generating devices ofthe present disclosure therefore preferably further comprise an ignitionpellet and/or primer. Suitable pellets and primers are known in the art.

The oxygen-generator, e.g. candle, may comprise several layers ofdifferent compositions and thus different reaction rates. Multiplelayers can be used to help match the oxygen generation requirements.Different applications have different oxygen generation requirements.The interface shapes and relative sizes and reactivities of the layerscan be modified, depending upon the requirements of the specificapplications of the oxygen-generating device.

The oxygen-generating devices of the present disclosure may thereforecomprise compositions in addition to the oxygen-generating compositionas herein described. Alternatively, the devices could comprise aplurality of layers comprising the same or different compositionsaccording to the present disclosure, e.g. layers comprisingoxygen-generating compositions as herein described which differ from oneanother in one or more aspects such as: the identity/amount of theoxygen source; the identity (e.g. specific proportion of metals in theoxide and/or degree of crystallinity)/amount of mixed-metal oxidepresent; and/or the amount and/or identity of any optional components asherein described.

Formation of devices according to the present disclosure may be achievedby preparing the mixed-metal oxide by any of the methods referred toherein and separately mixing the oxygen source with approximately 1 to 5wt. % water (the water being used as a lubricant to facilitate theformation of the oxygen-generating cores or candles). The mixed-metaloxide is then mixed with the wet oxygen source. The oxygen-generatingdevice, e.g. oxygen-generating candle, may be formed by compaction ofthe damp mixture in a mould, which is then dried, e.g. at about 120° C.,to remove the water that was added during the mixing process.

It will be appreciated that the disclosed uses and methods may takeadvantage of any of the materials described above in relation to thecompositions and products and vice versa.

All references herein to “comprising” should be understood to encompass“including” and “containing” as well as “consisting of” and “consistingessentially of”.

BRIEF DESCRIPTION OF THE DRAWINGS

One or more non-limiting examples will now be described, with referenceto the accompanying drawings, in which:

FIG. 1 shows a flow-chart outlining the method for preparing themixed-metal oxides of the present disclosure as described further inExample 1.

FIG. 2 shows decomposition of sodium chlorate using uncalcinated(Fe,Mg)O, according to Example 2.

FIG. 3 shows decomposition of lithium perchlorate using uncalcinated(Fe,Mg)O according to Example 3.

As shown in FIG. 1, mixed-metal oxides according to the presentdisclosure can be formed by precipitation. An aqueous solution ofMg(NO3)2.6H2O is prepared by dissolving Mg(NO3)2.6H2O in distilled H2O.A solution of Fe(NO3)3.9H2O is prepared in the same way. The nitratesolutions are concurrently added drop-wise to a stirred ammonia solutionwhile keeping the pH value above 11. The gelatinous precipitates can beseparated by centrifugation and rinsed with distilled H2O in a“cleansing” step. In order to produce nano-powder, the suspension can bequick-frozen using liquid nitrogen. Afterwards, it may be freeze-driedover at least 12 hours using a freeze-dryer. The combination the abovementioned precipitation, quick-freezing and freeze-drying steps producesnano-particles. Optionally a further crushing step may be used, althoughthe method allows production of nano-particles without any crushingstep.

It will be understood that the description above relates to anon-limiting example and that various changes and modifications may bemade from the arrangement shown without departing from the scope of thisdisclosure, which is set forth in the accompanying claims.

The disclosure will now be further described by way of the followingnon-limiting Examples:

EXAMPLE 1 Preparation of Mixed-Metal Oxides

Aqueous solutions of Mg(NO3)2.6H2O were prepared by dissolvingMg(NO3)2.6H2O in distilled H2O. A solution of Fe(NO3)3.9H2O was preparedin the same way. The nitrate solutions were concurrently added drop-wiseto a stirred ammonia solution while keeping the pH value above 11. Thegelatinous precipitates were rinsed with distilled H2O.

Finally, the solution was quick-frozen using liquid N₂. Afterwards, itwas freeze-dried over at least 72 hours using a freeze-dryer. (Fe,Mg)Osemi-crystalline powders were produced. Crystallinity<<10%. The ratio ofFe:Mg is determined by the preparation process.

EXAMPLE 2 Decomposition of Sodium Chlorate Using Uncalcinated (Fe,Mg)O

Uncalcinated nano-sized non-toxic (Fe,Mg)O (Fe 6 at. %) was preparedaccording to Example 1. It was combined with sodium chlorate (3 wt. %oxide with 97 wt. % sodium chlorate) by dry mixing (any method).

The decomposition of sodium chlorate alone and in the presence of eachof uncalcinated nano-sized non-toxic (Fe,Mg)O and cobalt oxide wasmonitored as reaction temperatures versus time and the results are shownin FIG. 2. The reaction heat developed in these reactions was determinedby themogravimetric differential scanning calorimetry (TG/DSC)measurements, recorded with heating rate of 10K/min in the temperaturerange from 20° C. to 700° C. The sample weight (NaClO3+(Fe,Mg)O) was40.0 mg.

The decomposition process of pure sodium chlorate starts at 500° C. andends at 600° C. (FIG. 2, dotted line). The decomposition process ofsodium chlorate in presence of uncalcinated nano-sized non-toxic(Fe,Mg)O starts at 390° C. and ends at 530° C. (FIG. 2, dashed line). Incomparison to what is considered one of the best catalysts, cobalt oxide(FIG. 2, solid line), the decomposition process using the oxide of thedisclosure is shifted to moderately higher temperature (about 100 Khigher). However, the mixed-metal oxide of the present disclosure alsoacts as a binder and fuel, thus removing the need for further componentsto perform these functions and is non-toxic, thus preferable to cobaltoxide, which is commonly considered to be the best catalyst for thisreaction.

EXAMPLE 3 Decomposition of Lithium Perchlorate Using Uncalcinated(Fe,Mg)O

Uncalcinated nano-sized non-toxic (Fe,Mg)O (Fe 6 at. %) was preparedaccording to Example 1. It was combined with lithium perchlorate (3 wt.% oxide with 97 wt. % sodium chlorate) by dry mixing (any method).

The decomposition of lithium perchlorate alone and in the presence ofeach of uncalcinated nano-sized non-toxic (Fe,Mg)O and cobalt oxide wasmonitored as reaction temperatures versus time and the results are shownin FIG. 3. The reaction heat developed in these reactions was determinedby themogravimetric differential scanning calorimetry (TG/DSC)measurements, recorded with heating rate of 10K/min in the temperaturerange from 20° C. to 700° C. The sample weight (LiClO4+(Fe,Mg)O) was40.0 mg.

The decomposition process of pure lithium perchlorate starts at 480° C.and ends at 510° C. (FIG. 3, dotted line). The decomposition process oflithium perchlorate in presence of uncalcinated nano-sized non-toxic(Fe,Mg)O starts at 420° C. and ends at 490° C. (FIG. 3, dashed line). Incomparison to what is considered one of the best catalysts, cobalt oxide(FIG. 3, solid line), the decomposition process using the oxide of thedisclosure is shifted to a slightly higher temperature, however, themixed-metal oxide of the present disclosure also acts as a binder andfuel, thus removing the need for further components to perform thesefunctions and is non-toxic, thus preferable to cobalt oxide, which iscommonly considered to be the best catalyst for this reaction.

1. An oxygen-generating composition comprising: an oxygen source and; amixed-metal oxide of formula: (Fe,Mg)O.
 2. The composition as claimed inclaim 1, wherein less than 25% of the mixed-metal oxide is crystalline.3. The composition as claimed in claim 1, wherein less than 10% of themixed-metal oxide is crystalline.
 4. The composition as claimed in claim1, wherein said mixed-metal oxide comprises 2 to 8 at. % Fe.
 5. Thecomposition as claimed in claim 1, wherein said mixed-metal oxide is inthe form of nano-particles.
 6. The composition as claimed in claim 5,wherein said nano-particles have a diameter of less than or equal to 500nm.
 7. The composition as claimed in claim 1, wherein said oxygen sourceis selected from alkali metal chlorates, alkali metal perchlorates,alkaline earth metal chlorates, alkaline earth metal perchlorates andmixtures thereof.
 8. The composition as claimed in claim 1, wherein saidoxygen source comprises sodium chlorate and/or lithium perchlorate. 9.The composition as claimed in claim 1, wherein said composition consistsessentially of said oxygen source and said mixed-metal oxide.
 10. Thecomposition as claimed in claim 1, wherein 90 to 99.9 wt. % of saidcomposition is said oxygen source.
 11. The composition as claimed inclaim 1, wherein 0.1 to 10 wt. % of said composition is said mixed-metaloxide.
 12. A method for generating oxygen, said method comprisingdecomposing an oxygen source as described in claim 1 in the presence ofa mixed-metal oxide.
 13. A chemical oxygen-generator comprising anoxygen-generating composition as claimed in claim
 1. 14. The chemicaloxygen-generator as claimed in claim 13, wherein said generatorcomprises a container for containing the oxygen-generating compositionand a primer for starting decomposition of the oxygen-generatingcomposition.
 15. The chemical oxygen-generator as claimed in claim 13wherein said chemical oxygen-generator is a chemical oxygen candle.